Stepwise Raw Synthesis Gas Purification via Selective Absorbent Segmentation

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Solution Overview

Problem

Conventional processes for separating accompanying gases from raw synthesis gas, such as the Rectisol process, face issues with the enrichment of aromatics and mercaptans in the absorbent, leading to premature degradation and environmental concerns due to the release of mercaptans during regeneration.

Innovation Solution

A stepwise separation process using a liquid absorbent countercurrently guided through all process steps, where aromatics and methyl mercaptans are separated in distinct absorption steps before the primary separation of H2S, COS, and CO2, with subsequent regeneration and washing to prevent mercaptan enrichment and odor nuisance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a single absorption step is used to separate H2S, COS, and CO2 from raw synthesis gas, then the process is simple and efficient for these components, but aromatics and mercaptans become enriched in the absorbent causing premature degradation and environmental problems

Engineering Contradiction:
Improveseparation efficiency of H2S, COS, CO2VSAvoidabsorbent service life
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The absorption process is divided into multiple sequential steps: first absorbing H2S, COS, and CO2 together, then performing a second absorption step to remove aromatics and mercaptans. This segmentation prevents harmful substances from accumulating in the absorbent, extending its service life while maintaining separation efficiency for the primary components.

Inventive Principle:
Principle #1Segmentation

2Productivity

If the absorbent is regenerated by depressurization or stripping, then CO2 and sulfur-containing gases are removed, but mercaptans are expelled together with CO2 causing odor nuisance to the environment

Engineering Contradiction:
Improveregeneration efficiencyVSAvoidmercaptan release
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The regeneration process is segmented into two distinct steps: first, depressurization or stripping removes CO2 and lighter gases; second, hot regeneration at elevated temperatures selectively removes sulfur-containing compounds including mercaptans. This segmented approach separates the release of different substances, preventing mercaptans from being expelled with CO2 and causing odor nuisance.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The regeneration process utilizes parameter changes, specifically temperature increase during hot regeneration, to selectively remove different substances at different stages. By changing the temperature parameter, mercaptans are effectively separated and removed in a controlled manner rather than being co-expelled with CO2 during depressurization.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If a selective absorption process is used to separate sulfur-containing gases and CO2 in separate steps, then the gases are kept separate during absorption, but additional absorption steps are required increasing process complexity

Engineering Contradiction:
Improvegas separation purityVSAvoidnumber of absorption steps
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The absorption process is segmented into functionally distinct steps: the first step absorbs H2S, COS, and CO2 together, while the second step specifically targets aromatics and mercaptans. This segmentation achieves high separation purity for different gas groups while organizing the complexity into a systematic, manageable sequence of operations.

Inventive Principle:
Principle #1Segmentation

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This process extends the absorbent's service life, reduces environmental impact by separating mercaptans effectively, and maintains the purity of sulfur-containing gases for further processing, particularly in coal gasification-derived synthesis gas streams.

Implementation Method 1

separation of accompanying gases from a raw synthesis gas stream by a liquid absorbent countercurrently guided through all process steps

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Implementation Method 2

In a first regeneration step CO2 is removed from the loaded methanol absorbent by depressurization and/or stripping with a gas

Methodology Applied
Scientific EffectDepressurization: Depressurisation

Implementation Method 3

In a first regeneration step CO2 is removed from the loaded methanol absorbent by depressurization and/or stripping with a gas

Methodology Applied
Scientific EffectStripping: Sparging

Implementation Method 4

In a second regeneration step the sulfur-containing gases, COS and H2S, are expelled by heating

Methodology Applied
Scientific EffectHeating: Heating

Data Source

PatentEP3229939B1Process and plant for the purification of raw synthesis gas
Publication Date: 2020.06.10 LAIR LIQUIDE SA POUR LETUDE & LEXPLOITATION DES PROCEDES GEORGES CLAUDE
  • EP3229939B1 patent drawingFigure 1

AI summary

A process for the stepwise separation of accompanying gases from a raw synthesis gas stream by a liquid absorbent countercurrently guided through all process steps and circulated via regeneration plants, wherein either the accompanying gases H2S, COS and CO2 are separated in a common absorption step or, in one of the selective absorption steps chiefly H2S and COS are separated and in the next step in flow direction of the gas chiefly CO2 is separated, and in the last step a separation of accompanying gas residues (fine wash) is effected, wherein before the separation of H2S and COS an absorption step chiefly for the separation of aromatics and subsequently an absorption step chiefly for the separation of methyl mercaptan is carried out.